DE69811113D1 - Herstellung eines synthesegases mit niedrigem wasserstoffgehalt unter verwendung von co2 und einem nickelkatalysator - Google Patents
Herstellung eines synthesegases mit niedrigem wasserstoffgehalt unter verwendung von co2 und einem nickelkatalysatorInfo
- Publication number
- DE69811113D1 DE69811113D1 DE69811113T DE69811113T DE69811113D1 DE 69811113 D1 DE69811113 D1 DE 69811113D1 DE 69811113 T DE69811113 T DE 69811113T DE 69811113 T DE69811113 T DE 69811113T DE 69811113 D1 DE69811113 D1 DE 69811113D1
- Authority
- DE
- Germany
- Prior art keywords
- production
- synthesis gas
- nickel catalyst
- low hydrogen
- hydrogen synthesis
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
- C01B3/42—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts using moving solid particles
- C01B3/44—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts using moving solid particles using the fluidised bed technique
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1041—Composition of the catalyst
- C01B2203/1047—Group VIII metal catalysts
- C01B2203/1052—Nickel or cobalt catalysts
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1041—Composition of the catalyst
- C01B2203/1082—Composition of support materials
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1205—Composition of the feed
- C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
- C01B2203/1235—Hydrocarbons
- C01B2203/1241—Natural gas or methane
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Catalysts (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/961,814 US5985178A (en) | 1997-10-31 | 1997-10-31 | Low hydrogen syngas using CO2 and a nickel catalyst |
PCT/US1998/023340 WO1999023030A1 (en) | 1997-10-31 | 1998-10-30 | Low hydrogen syngas using co2 and a nickel catalyst |
Publications (2)
Publication Number | Publication Date |
---|---|
DE69811113D1 true DE69811113D1 (de) | 2003-03-06 |
DE69811113T2 DE69811113T2 (de) | 2003-11-13 |
Family
ID=25505056
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE69811113T Expired - Fee Related DE69811113T2 (de) | 1997-10-31 | 1998-10-30 | Herstellung eines synthesegases mit niedrigem wasserstoffgehalt unter verwendung von co2 und einem nickelkatalysator |
Country Status (8)
Country | Link |
---|---|
US (1) | US5985178A (de) |
EP (1) | EP1034133B1 (de) |
AU (1) | AU737328B2 (de) |
BR (1) | BR9813343A (de) |
CA (1) | CA2308285A1 (de) |
DE (1) | DE69811113T2 (de) |
NO (1) | NO20002269L (de) |
WO (1) | WO1999023030A1 (de) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6168768B1 (en) * | 1998-01-23 | 2001-01-02 | Exxon Research And Engineering Company | Production of low sulfer syngas from natural gas with C4+/C5+ hydrocarbon recovery |
DE19833644C2 (de) * | 1998-07-25 | 2002-06-13 | Xcellsis Gmbh | Reaktoreinheit in einem System zur Erzeugung eines wasserstoffreichen Gases aus einem flüssigen Rohkraftstoff |
US6946111B2 (en) * | 1999-07-30 | 2005-09-20 | Conocophilips Company | Short contact time catalytic partial oxidation process for recovering sulfur from an H2S containing gas stream |
US7326397B2 (en) * | 2000-12-18 | 2008-02-05 | Conocophillips Company | Catalytic partial oxidation process for recovering sulfur from an H2S-containing gas stream |
US7357908B2 (en) * | 2000-12-18 | 2008-04-15 | Conocophillips Company | Apparatus and catalytic partial oxidation process for recovering sulfur from an H2S-containing gas stream |
US7491250B2 (en) * | 2002-06-25 | 2009-02-17 | Exxonmobil Research And Engineering Company | Pressure swing reforming |
US20040170559A1 (en) * | 2003-02-28 | 2004-09-02 | Frank Hershkowitz | Hydrogen manufacture using pressure swing reforming |
US7914764B2 (en) * | 2003-02-28 | 2011-03-29 | Exxonmobil Research And Engineering Company | Hydrogen manufacture using pressure swing reforming |
US7217303B2 (en) * | 2003-02-28 | 2007-05-15 | Exxonmobil Research And Engineering Company | Pressure swing reforming for fuel cell systems |
US7108842B2 (en) * | 2004-01-15 | 2006-09-19 | Conocophillips Company | Process for the catalytic partial oxidation of H2S using staged addition of oxygen |
US7226572B1 (en) | 2006-03-03 | 2007-06-05 | Conocophillips Company | Compact sulfur recovery plant and process |
US7501111B2 (en) | 2006-08-25 | 2009-03-10 | Conoco Phillips Company | Increased capacity sulfur recovery plant and process for recovering elemental sulfur |
US20100327231A1 (en) * | 2009-06-26 | 2010-12-30 | Noah Whitmore | Method of producing synthesis gas |
US20110039686A1 (en) * | 2009-08-14 | 2011-02-17 | Battelle Memorial Institute | Fast regeneration of sulfur deactivated Ni-based hot biomass syngas cleaning catalysts |
US10369549B2 (en) | 2015-03-20 | 2019-08-06 | Sabic Global Technologies B.V. | Use of nickel-manganese olivine and nickel-manganese spinel as bulk metal catalysts for carbon dioxide reforming of methane |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR367654A (fr) * | 1906-05-19 | 1906-11-07 | Watzlaw De Czapiewski | Fraiseuse à main |
GB8520567D0 (en) * | 1985-08-16 | 1985-09-25 | British Petroleum Co Plc | Production of synthesis gas |
US4888131A (en) * | 1988-03-28 | 1989-12-19 | Exxon Research And Engineering Company | Synthesis gas preparation and catalyst therefor |
CA1333008C (en) * | 1988-03-28 | 1994-11-15 | Duane Arlen Goetsch | Synthesis gas preparation and catalyst therefor |
US4877550A (en) * | 1988-03-28 | 1989-10-31 | Exxon Research And Engineering Company | Synthesis gas preparation and catalyst therefor |
FR2638443B1 (fr) * | 1988-11-03 | 1991-01-11 | Inst Francais Du Petrole | Procede pour la production de gaz de synthese par oxydation partielle d'hydrocarbures legers |
IT1238676B (it) * | 1990-01-26 | 1993-09-01 | Snam Progetti | Sistema catalitico e procedimento per la produzione di gas di sintesi mediante reazione di reforming di idrocarubri leggeri con co2 |
GB9028034D0 (en) * | 1990-12-24 | 1991-02-13 | Isis Innovation | Improved processes for the conversion of methane to synthesis gas |
US5160456A (en) * | 1991-06-07 | 1992-11-03 | Exxon Research And Engineering Company | Catalyst/heat-transfer medium for syngas generation |
US5143647A (en) * | 1991-06-07 | 1992-09-01 | Exxon Research And Engineering Company | Synthesis gas generation startup process (C-2556) |
IT1256227B (it) * | 1992-12-23 | 1995-11-29 | Snam Progetti | Procedimento catalitico per la produzione di gas di sintesi |
CA2143962A1 (en) * | 1994-03-25 | 1995-09-26 | David Chester Long | Synthesis gas preparation by partial oxidation-steam reforming |
CA2156882A1 (en) * | 1994-09-06 | 1996-03-07 | Frederick John Kaiser Jr. | Process for selective catalyst particle size control by ex situ grinding to maintain bed fluidization during high temperature operations |
US5421840A (en) * | 1994-09-06 | 1995-06-06 | Exxon Research And Engineering Company | Production of synthesis gas via fluidized bed/fixed bed process combination |
-
1997
- 1997-10-31 US US08/961,814 patent/US5985178A/en not_active Expired - Fee Related
-
1998
- 1998-10-30 BR BR9813343-8A patent/BR9813343A/pt not_active Application Discontinuation
- 1998-10-30 DE DE69811113T patent/DE69811113T2/de not_active Expired - Fee Related
- 1998-10-30 AU AU13004/99A patent/AU737328B2/en not_active Ceased
- 1998-10-30 WO PCT/US1998/023340 patent/WO1999023030A1/en active IP Right Grant
- 1998-10-30 EP EP98956488A patent/EP1034133B1/de not_active Expired - Lifetime
- 1998-10-30 CA CA002308285A patent/CA2308285A1/en not_active Abandoned
-
2000
- 2000-04-28 NO NO20002269A patent/NO20002269L/no not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
NO20002269L (no) | 2000-06-23 |
BR9813343A (pt) | 2000-08-22 |
WO1999023030A1 (en) | 1999-05-14 |
CA2308285A1 (en) | 1999-05-14 |
EP1034133A1 (de) | 2000-09-13 |
WO1999023030A9 (en) | 1999-08-12 |
US5985178A (en) | 1999-11-16 |
AU1300499A (en) | 1999-05-24 |
DE69811113T2 (de) | 2003-11-13 |
AU737328B2 (en) | 2001-08-16 |
EP1034133B1 (de) | 2003-01-29 |
NO20002269D0 (no) | 2000-04-28 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE69811113D1 (de) | Herstellung eines synthesegases mit niedrigem wasserstoffgehalt unter verwendung von co2 und einem nickelkatalysator | |
DE69329455D1 (de) | Verfahren zur herstellung von synthesegas unter verwendung von nickel-katalysatoren | |
DE69801053D1 (de) | Autothermer reaktor mit einer sauerstoffionen leitenden dichten keramischen membran und dessen verwendung in einem verfahren zur erzeugung von synthesegas | |
DE59400996D1 (de) | Katalysator, dessen Herstellung und Verwendung zur Gasphasenpolymerisation von konjugierten Dienen | |
DE69808729D1 (de) | Methode zur herstellung und verwendung eines nickelkatalysators | |
DE69913429D1 (de) | Reaktor mit einer Keramikmembran zur Herstellung von Synthesegas | |
ATE270584T1 (de) | Verfahren zur gewinnung von synthesegas mittels eines nickel- und rhodiumhaltiger katalysators | |
DE69525852D1 (de) | Verfahren zur herstellung von methanol unter verwendung eines einen hohen stickstoffgehalt aufweisenden synthesengases mit wasserstoffrückführung | |
DE69626542D1 (de) | Brenner und seine Verwendung zur Herstellung von Synthesegas | |
DE69801657D1 (de) | Slurrykohlenwasserstoffsynthese mit cyklischer abführung von co und katalysatorwiederbelebung | |
DE69913213D1 (de) | Integration von einem kryogenen Lufttrenner mit Synthesegasherstellung und Konvertierung | |
NO20004054L (no) | Gassomdannelse som anvender syntesegass fremstilt av hydrogen for katalysatorregenerering og hydrokarbonomdannelse | |
DE59500837D1 (de) | Verfahren zur Herstellung von Acetylen und Synthesegas | |
DE69723301D1 (de) | Einstufige umsetzung von methanol zu wasserstoff und kohlendioxid | |
DE69808751D1 (de) | Kohlenwasserstoffsynthese unter verwendung von restgasen zur katalysatorwiederbelebung | |
NO971609D0 (no) | Fremgangsmåte for omvandling av syntesegass i nærvær av en katalysator basert på kobolt og titan | |
GB2240284B (en) | Catalytic system and process for producing synthesis gas by reforming light hydrocarbons with co2 | |
FR2694013B1 (fr) | Catalyseur à base de cobalt et procédé de conversion du gaz de synthèse en hydrocarbures. | |
DE69407692D1 (de) | Benutzung eines Nickelträgerkatalysators zur Dampfreformierung | |
DE69300627D1 (de) | Verfahren und Reaktor zur Herstellung von wasserstoff- und kohlenmonoxidreichem Gas. | |
DE69829248D1 (de) | Kryogenische Einstellung vom Wasserstoff/Kohlenoxydgehalt von Synthesegas | |
DE59403037D1 (de) | Verwendung eines katalysators zur herstellung von synthesegas | |
AU7158287A (en) | Method for the catalytic production of methane from a synthesis gas containing carbon monoxide, carbon dioxide and hydrogen, and reactor for carrying out the method | |
GB2236262B (en) | Catalyst for conversion of synthesis gas into hydrocarbons | |
NO964018D0 (no) | Fremgangsmåte for omdannelse av syntesegass i nærvær av en katalysator som omfatter kobolt og ytterligere elementer |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
8364 | No opposition during term of opposition | ||
8339 | Ceased/non-payment of the annual fee |